Shear-Thinning Properties of Blood in Large Arteries

Newtonian and non-Newtonian viscous models have been widely applied in many biofluid research areas in order to understand the relationship between hemodynamics and vascular disease. Using Newtonian blood in modeling blood flow for large arteries in cardiovascular hemodynamics has become a common assumption in much of the literature. However, the criteria of size and flow regime that are suitable for such an assumption have not been very well defined. This study reviews the difference between two of the most commonly used viscous blood-flow models found in the literature: the Newtonian model with a constant dynamic blood viscosity of  = 0.0035 Pa∙s, and the Carreau-Yasuda nonNewtonian model, which accounts for the shear-thinning properties of blood. CFD simulations were conducted under steady-state and transient-state conditions in a straight tube flow. For the steady-state condition, tube diameters in the range of 2 to 16 cm were tested with Reynolds numbers in the range of 520 < Re < 1560. For the transient-state condition, flow was characterized with a mean Reynolds number Remean = 520 and a Womersley number in the range of 10.00 < < 27.59. Results suggest that the difference between the shear-thinning non-Newtonian model and the Newtonian model is increased under flow conditions where reversed flow is expected. However, such a difference is reduced when the  increases.

[1]  Alessandro Bottaro,et al.  Delaying transition to turbulence in channel flow: revisiting the stability of shear-thinning fluids , 2007, Journal of Fluid Mechanics.

[2]  A. Yoganathan,et al.  Biofluid Mechanics: The Human Circulation , 2006 .

[3]  F. Pinho,et al.  Vortex shedding in cylinder flow of shear-thinning fluids I. Identification and demarcation of flow regimes , 2003 .

[4]  van de Fn Frans Vosse,et al.  The influence of the non-Newtonian properties of blood on the flow in large arteries: unsteady flow in a 90° curved tube , 1999 .

[5]  T. Muto,et al.  Unsteady Flow in Circular Tube : Velocity Distribution of Pulsating Flow , 1980 .

[6]  B. W. Martin,et al.  Developing laminar flow in a pipe of circular cross-section , 1971, Proceedings of the Royal Society of London. A. Mathematical and Physical Sciences.

[7]  E. Merrill,et al.  Viscosity of human blood: transition from Newtonian to non-Newtonian. , 1967, Journal of applied physiology.

[8]  F. Pinho,et al.  Vortex shedding in cylinder flow of shear-thinning fluids. III , 2004 .

[9]  Fjh Frank Gijsen Modeling of wall shear stress in large arteries , 1998 .

[10]  J. Tarbell,et al.  Flow of non-Newtonian blood analog fluids in rigid curved and straight artery models. , 1990, Biorheology.

[11]  D. Ku,et al.  The effects of non-Newtonian viscoelasticity and wall elasticity on flow at a 90° bifurcation , 1986 .

[12]  D Liepsch,et al.  Pulsatile flow of non-Newtonian fluid in distensible models of human arteries. , 1984, Biorheology.

[13]  D. Liepsch,et al.  Flow investigations in a model of a three-dimensional human artery with Newtonian and non-Newtonian fluids. Part I. , 1983, Biorheology.